US20030200865A1 - Reduced noise oxygen concentrator - Google Patents

Reduced noise oxygen concentrator Download PDF

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US20030200865A1
US20030200865A1 US10/421,259 US42125903A US2003200865A1 US 20030200865 A1 US20030200865 A1 US 20030200865A1 US 42125903 A US42125903 A US 42125903A US 2003200865 A1 US2003200865 A1 US 2003200865A1
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module assembly
components
oxygen
gas
blower fan
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US6908503B2 (en
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Norman McCombs
James Alessi
Rober Casey
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Caire Inc
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Airsep Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0415Beds in cartridges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/047Pressure swing adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/106Silica or silicates
    • B01D2253/108Zeolites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2256/00Main component in the product gas stream after treatment
    • B01D2256/12Oxygen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/10Single element gases other than halogens
    • B01D2257/102Nitrogen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40011Methods relating to the process cycle in pressure or temperature swing adsorption
    • B01D2259/40077Direction of flow
    • B01D2259/40081Counter-current
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40083Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
    • B01D2259/40086Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/402Further details for adsorption processes and devices using two beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/45Gas separation or purification devices adapted for specific applications
    • B01D2259/4533Gas separation or purification devices adapted for specific applications for medical purposes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/45Gas separation or purification devices adapted for specific applications
    • B01D2259/455Gas separation or purification devices adapted for specific applications for transportable use
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0438Cooling or heating systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0446Means for feeding or distributing gases

Definitions

  • the present invention relates generally to an oxygen concentration apparatus, and more particularly to the concentration of oxygen by pressure swing adsorption.
  • PSA pressure swing adsorption technique
  • the oxygen concentrator is a device used to concentrate oxygen out of ambient air and to supply the oxygen concentrated mixture for medical or other purposes, where an oxygen rich gas is required.
  • the general type and operating principles of PSA apparatus with which this invention is concerned are described in U.S. Pat. Nos. 3,564,816; 3,636,679; 3,717,974; 4,802,899; 5,531,807 and 5,871,564, among others.
  • a pressure swing adsorption apparatus may include one or more adsorbers, each having a fixed sieve bed of adsorbent material to fractionate at least one constituent gas from a gaseous mixture by adsorption into the bed, when the gaseous mixture from a feed stream is sequentially directed through the adsorbers in a co-current direction. While one adsorber performs adsorption, another adsorber is simultaneously purged of its adsorbed constituent gas by part of the product gas that is withdrawn from the first or producing adsorber and directed through the other adsorber in a counter-current direction.
  • the feed stream at a preset time is then directed to the other adsorber in the co-current direction, so that the other adsorber performs adsorption.
  • the first adsorber then is purged either simultaneously, or in another timed sequence if there are more than two adsorbers, all of which will be understood from a reading of the above described patents. While oxygen concentrators have proven to be very useful for many medical and other applications, those known to us will generate a noise level than can limit their usefulness in many environments, such as public locations or at health treatment facilities.
  • the compact size of this device requires internal components to be tightly packed and in close proximity of each other. While the compact size of the device gives the apparatus a distinct advantage, difficulty may be experienced in repair or maintenance. Removal or repair of a particular component often requires the removal of surrounding components so that access may be obtained.
  • the present invention provides a new and improved pressure swing adsorption (“PSA” or “oxygen concentrator”) apparatus that can operate at a lower noise level than prior art oxygen concentrators and facilitates access to internal components. This is accomplished by a unique configuration of internal components combined with strategic placement of sound deadening material.
  • the prior art oxygen concentrators as known to us operate, for example, at noise levels of between about 48 and 54 decibels.
  • the oxygen concentrator of the present invention will operate at a significantly lower noise level of about 38 decibels, and even lower.
  • This improvement is accomplished by the strategic placement of noise absorbing material and rearrangement of the physical layout of the major noise-generating components in a removable module within the overall housing or cabinet of the PSA apparatus.
  • the removable module serves as an advantage during maintenance and repair because all major components thus become easily accessible upon removal of the module.
  • the component assembly and receiving cabinet can be standardized, such that multiple models can be furnished to meet customer demand through the substitution of various module assemblies.
  • the module assembly contains virtually all of the noisier items of a PSA apparatus, including the air flow generating fan, the resonator and compressor used to intake air to be fractionated, the valves controlling the gas flow through the adsorber beds, and the exhaust muffler.
  • the noise reducing qualities of this device are further enhanced by the addition of at least one layer of sound absorbing material positioned between the outer walls of the module and the adjacent walls of the outer housing and internal components not contained within the module. This sound absorbing material will attenuate structure borne vibration, reducing radiated noise, as well as absorb airborne sound.
  • FIG. 1 is a schematic illustration of a combined PSA apparatus according to the invention
  • FIG. 2 is a front view of the reduced noise oxygen concentrator with the front panel of component module assembly removed.
  • FIG. 3 is a back view of the reduced noise oxygen concentrator with its back cover removed.
  • FIG. 4 is an isometric view of the component module assembly from the front and top, without the noise reducing material.
  • FIG. 5 a and FIG. 5 b are detailed drawings of the fan mounted to the fan assembly panel.
  • FIG. 6 is a side view of the component module assembly with side cover removed.
  • a pressure swing adsorption apparatus used for fractionating at least one component, namely nitrogen, from a gaseous mixture, generally but not necessarily ambient air, by pressure swing adsorption to produce a product gas.
  • a gaseous mixture generally but not necessarily ambient air
  • pressure swing adsorption apparatus used for fractionating at least one component, namely nitrogen, from a gaseous mixture, generally but not necessarily ambient air, by pressure swing adsorption to produce a product gas.
  • the invention as described uses two nitrogen adsorbers, it may also be incorporated into PSA apparatus using one or more than two adsorbers.
  • ambient air is supplied to the PSA apparatus 20 through a filtered intake 21 and an intake resonator 22 to decrease the noise from the intake of the ambient air feed stream.
  • the feed stream continues from resonator 22 and is moved from its outlet 22 a by a feed air compressor/heat exchanger assembly 24 alternatively to first and second adsorbers 30 , 32 through feed valves 40 and 42 respectively.
  • Compressor/heat exchanger assembly 24 as shown includes a compressor 24 a with an air inlet 24 c and an outlet 24 d followed by the heat exchanger 24 b.
  • Ambient air is supplied to the apparatus 20 by a fan 63 used to draw air into the interior of the apparatus 20 , a portion of which air is drawn into the filtered intake 21 and the majority of which is directed throughout the interior of the apparatus to cool the operating components.
  • the respective adsorber fractionates the feed stream into the desired concentration of product gas.
  • the adsorbent material used for the beds to separate nitrogen from the ambient air may be a synthetic zeolite or other known adsorber material having equivalent properties.
  • the substantial or usable portion of the oxygen enriched product gas generated by the ambient air flowing in the co-current direction sequentially in each one of the absorbers 30 , 32 is directed through the outlet 30 b , 32 b and check valve 34 , 36 of the corresponding adsorber to a product manifold 48 from where it is delivered to a mixing tank 56 .
  • the product gas is delivered through a bacteria filter 57 to a user outlet at a regulated pressure and flow rate as determined by a flow controller 59 and a pressure regulator 58 .
  • the balance of the product gas generated by each adsorber is timed to be diverted through a purge orifice 50 and a properly timed equalization valve 52 and an optional flow restrictor 53 to flow through the other adsorber 30 or 32 in the counter-current direction from the respective outlet 30 b , 32 b and to the respective inlet 30 a , 32 a of the other adsorber to purge the adsorbed, primarily nitrogen, gases.
  • the counter-current product gas and purged gases then are discharged to the atmosphere from the adsorbers through properly timed waste valves 44 , 46 , tubing 47 and a sound absorbing muffler 48 .
  • the principal noise generating components are the fan 63 , intake resonator 22 , the compressor/heat exchanger assembly 24 , the feed and waste valves 40 , 42 , 44 , 46 , and sound absorbing muffler 48 , these components according to the invention are mounted in a separate, removable module assembly 60 as will be described.
  • FIG. 2 a front view of the reduced noise oxygen concentrator 20 is shown.
  • the operating components of the apparatus are enclosed within an outer housing or cabinet 25 , the front cover of which has been removed from this view to illustrate component module assembly 60 .
  • Attached to the outer surface of the module side walls 61 at both sides and the top wall 69 is a layer of sound deadening material 74 .
  • a fan assembly panel 66 is also shown in FIG. 2 .
  • a layer of sound deadening material is shown to be attached to the inner surface of the back wall 67 of the cabinet superstructure (not shown), where the outer surface of the back wall 67 of the module assembly 60 meets the inner surface of the back wall.
  • the working components shown to be mounted on the front side of the concentrator 20 within module 60 include intake resonator 22 , fan 63 , a valve block 64 forming the feed and waste valves 40 , 42 , 44 , 46 , and waste muffler 48 .
  • the working components of the back side of the concentrator as illustrated in FIG. 3 and partially in FIG. 2 include the pair of adsorbers 30 and 32 , equalization valve 52 , a circuit board 70 containing the electronic components that control the operating sequence of the apparatus 20 , and compressor assembly 24 .
  • the compressor 24 is mounted to the bottom wall 62 of module 60 by means of the appropriate screws or other suitable fastening devices.
  • the valve block 64 is disposed within module 60 immediately below and in front of the compressor assembly 24 .
  • the valve block 64 may suitably be attached to bottom wall 62 by means of a quick release fastener, such as VelcroTM.
  • the feed valves 30 a , 32 a are in the flow path between the heat exchanger 24 b and the adsorber inlets 30 a , 32 a by suitable tubing which at 71 and 72 are connected by detachable couplings to enable removal of the module 60 .
  • the electrical connections between the operating components within the module 60 on the one hand, and the power source and circuit board 70 on the other hand also are made by detachable bus connections in a manner well known in the art.
  • the intake resonator 22 Immediately above the bottom wall 62 of module 60 is the intake resonator 22 .
  • the intake resonator 22 is mounted in close proximity to fan 63 to receive through filtered intake 21 (not shown) the portion of air to be fractionated.
  • Ambient air is drawn into housing 25 by a suitable louvered opening (not shown) in the rear wall 67 of housing 25 .
  • the upper wall 69 of component module assembly 60 has an opening 65 coinciding with the internal fan panel 66 .
  • the fan panel 66 is mounted at about a 20° angle so that fan 63 draws air from inside housing 25 into the component module assembly 60 to be directed partially into intake 21 and the balance over the operating components within module 60 before exiting through an opening at the back wall of module 60 .
  • the fan and compressor have been repositioned within the walls of the module to further reduce the noise level. This is accomplished by positioning the compressor substantially toward the back wall, opposing the fan panel 66 .
  • FIG. 4 further illustrates the opening 65 in the top of the module 60 adjacent to the fan 63 .
  • FIG. 5 a and FIG. 5 b provide two views of the fan 63 and fan panel 66 and. further illustrate the means and angle by which fan 63 mounted to the fan panel 66 .
  • FIG. 5 b further illustrates a layer of sound absorbing material 75 between the fan assembly panel 66 and the fan 63 .
  • the fan assembly panel 66 is then mounted between the sidewalls, angularly facing the opening in the upper wall.
  • the noise reducing qualities of this device are further enhanced by the addition of a layer of sound absorbing material 75 . This sound absorbing material will attenuate structure borne vibration and reduce radiated noise.
  • Suitable openings are provided in the modules walls, as for example bottom wall 62 and back wall 67 of the component module assembly 60 where the circulating air cooling the contained components and the waste gas from muffler 48 exit the component module assembly.
  • FIG. 6 is a the side view of the component module assembly with side cover removed.
  • the figure particularly illustrates a compressor 24 mounted in close proximity to the back wall 67 of the component module assembly.
  • the figure also illustrates a side view of the fan panel 66 , mounted in close proximity to the front wall 68 of the component module assembly. Sounds normally associated with the discharging of a pressurized stream of gas to the atmosphere are muffled by the silencer 48 .

Abstract

A pressure swing adsorption apparatus for producing a gas mixture with a higher concentration of a particular gas such as oxygen from ambient air, in which the noisier components of the apparatus are contained in an internal removable module that is separated by sound insulation from the balance the apparatus to attenuate structure borne vibration, reduce radiated noise, and to absorb airborne sound.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • This application claims priority from a U.S. Provisional Patent Application, Serial No. 60/375,256, filed Apr. 24, 2002.[0001]
  • FIELD OF THE INVENTION
  • The present invention relates generally to an oxygen concentration apparatus, and more particularly to the concentration of oxygen by pressure swing adsorption. [0002]
  • BACKGROUND OF THE INVENTION
  • Various types of equipment are known to provide patients with oxygen or oxygen-enriched air supplies in order to sustain life-support systems or relieve symptoms of various types of debilitating diseases, particularly of the lungs. In the past, pure oxygen or oxygen-enriched gases supplied from pressurized cylinders have been used. However, such cylinders are cumbersome and have a relatively short life before they need to be refilled or replaced. Oxygen concentrators using the principle of pressure swing adsorption were designed to overcome these obstacles. [0003]
  • Generally, the pressure swing adsorption technique, hereinafter referred to as PSA, is used to concentrate a selected gas out of a mixture of gases. Particularly, the oxygen concentrator is a device used to concentrate oxygen out of ambient air and to supply the oxygen concentrated mixture for medical or other purposes, where an oxygen rich gas is required. The general type and operating principles of PSA apparatus with which this invention is concerned are described in U.S. Pat. Nos. 3,564,816; 3,636,679; 3,717,974; 4,802,899; 5,531,807 and 5,871,564, among others. For example, a pressure swing adsorption apparatus may include one or more adsorbers, each having a fixed sieve bed of adsorbent material to fractionate at least one constituent gas from a gaseous mixture by adsorption into the bed, when the gaseous mixture from a feed stream is sequentially directed through the adsorbers in a co-current direction. While one adsorber performs adsorption, another adsorber is simultaneously purged of its adsorbed constituent gas by part of the product gas that is withdrawn from the first or producing adsorber and directed through the other adsorber in a counter-current direction. Once the other adsorber is purged, the feed stream at a preset time is then directed to the other adsorber in the co-current direction, so that the other adsorber performs adsorption. The first adsorber then is purged either simultaneously, or in another timed sequence if there are more than two adsorbers, all of which will be understood from a reading of the above described patents. While oxygen concentrators have proven to be very useful for many medical and other applications, those known to us will generate a noise level than can limit their usefulness in many environments, such as public locations or at health treatment facilities. [0004]
  • Additionally, the compact size of this device requires internal components to be tightly packed and in close proximity of each other. While the compact size of the device gives the apparatus a distinct advantage, difficulty may be experienced in repair or maintenance. Removal or repair of a particular component often requires the removal of surrounding components so that access may be obtained. [0005]
  • Therefore, what is needed in the art is a compact and mobile oxygen concentrator with reduced noise. [0006]
  • Furthermore, what is needed in the art is an oxygen concentrator with easily accessible components to assist in maintenance and repair. [0007]
  • SUMMARY OF THE INVENTION
  • The present invention provides a new and improved pressure swing adsorption (“PSA” or “oxygen concentrator”) apparatus that can operate at a lower noise level than prior art oxygen concentrators and facilitates access to internal components. This is accomplished by a unique configuration of internal components combined with strategic placement of sound deadening material. The prior art oxygen concentrators as known to us operate, for example, at noise levels of between about 48 and 54 decibels. The oxygen concentrator of the present invention will operate at a significantly lower noise level of about 38 decibels, and even lower. This improvement is accomplished by the strategic placement of noise absorbing material and rearrangement of the physical layout of the major noise-generating components in a removable module within the overall housing or cabinet of the PSA apparatus. The removable module serves as an advantage during maintenance and repair because all major components thus become easily accessible upon removal of the module. Also, from a manufacturing standpoint, the component assembly and receiving cabinet can be standardized, such that multiple models can be furnished to meet customer demand through the substitution of various module assemblies. [0008]
  • The module assembly contains virtually all of the noisier items of a PSA apparatus, including the air flow generating fan, the resonator and compressor used to intake air to be fractionated, the valves controlling the gas flow through the adsorber beds, and the exhaust muffler. The noise reducing qualities of this device are further enhanced by the addition of at least one layer of sound absorbing material positioned between the outer walls of the module and the adjacent walls of the outer housing and internal components not contained within the module. This sound absorbing material will attenuate structure borne vibration, reducing radiated noise, as well as absorb airborne sound.[0009]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The above-mentioned and other features and advantages of this invention, and the manner of attaining them, will become apparent and be more completely understood by reference to the following description of a preferred embodiment of the invention when read in conjunction with the accompanying drawings, wherein: [0010]
  • FIG. 1 is a schematic illustration of a combined PSA apparatus according to the invention; [0011]
  • FIG. 2 is a front view of the reduced noise oxygen concentrator with the front panel of component module assembly removed. [0012]
  • FIG. 3 is a back view of the reduced noise oxygen concentrator with its back cover removed. [0013]
  • FIG. 4 is an isometric view of the component module assembly from the front and top, without the noise reducing material. [0014]
  • FIG. 5[0015] a and FIG. 5b are detailed drawings of the fan mounted to the fan assembly panel.
  • FIG. 6 is a side view of the component module assembly with side cover removed.[0016]
  • Corresponding reference characters indicate corresponding parts throughout the several views. Although a preferred embodiment is illustrated and described, it is not to be construed as limiting the scope of the invention in any manner. [0017]
  • DETAILED DESCRIPTION OF INVENTION
  • Turning now to the drawings and in accordance with the present invention, there is shown a specific embodiment, generally indicated as [0018] 20, of a pressure swing adsorption apparatus, used for fractionating at least one component, namely nitrogen, from a gaseous mixture, generally but not necessarily ambient air, by pressure swing adsorption to produce a product gas. Although the invention as described uses two nitrogen adsorbers, it may also be incorporated into PSA apparatus using one or more than two adsorbers.
  • With reference to FIG. 1, ambient air is supplied to the [0019] PSA apparatus 20 through a filtered intake 21 and an intake resonator 22 to decrease the noise from the intake of the ambient air feed stream. The feed stream continues from resonator 22 and is moved from its outlet 22 a by a feed air compressor/heat exchanger assembly 24 alternatively to first and second adsorbers 30, 32 through feed valves 40 and 42 respectively. Compressor/heat exchanger assembly 24 as shown includes a compressor 24 a with an air inlet 24 c and an outlet 24 d followed by the heat exchanger 24 b.
  • Ambient air is supplied to the [0020] apparatus 20 by a fan 63 used to draw air into the interior of the apparatus 20, a portion of which air is drawn into the filtered intake 21 and the majority of which is directed throughout the interior of the apparatus to cool the operating components.
  • When the feed stream alternatively enters [0021] inlets 30 a, 32 a of adsorbers 30, 32 in a co-current direction, the respective adsorber fractionates the feed stream into the desired concentration of product gas. The adsorbent material used for the beds to separate nitrogen from the ambient air may be a synthetic zeolite or other known adsorber material having equivalent properties.
  • The substantial or usable portion of the oxygen enriched product gas generated by the ambient air flowing in the co-current direction sequentially in each one of the [0022] absorbers 30, 32 is directed through the outlet 30 b, 32 b and check valve 34, 36 of the corresponding adsorber to a product manifold 48 from where it is delivered to a mixing tank 56. From mixing tank 56, the product gas is delivered through a bacteria filter 57 to a user outlet at a regulated pressure and flow rate as determined by a flow controller 59 and a pressure regulator 58. The balance of the product gas generated by each adsorber is timed to be diverted through a purge orifice 50 and a properly timed equalization valve 52 and an optional flow restrictor 53 to flow through the other adsorber 30 or 32 in the counter-current direction from the respective outlet 30 b, 32 b and to the respective inlet 30 a, 32 a of the other adsorber to purge the adsorbed, primarily nitrogen, gases. The counter-current product gas and purged gases then are discharged to the atmosphere from the adsorbers through properly timed waste valves 44, 46, tubing 47 and a sound absorbing muffler 48.
  • As the principal noise generating components are the [0023] fan 63, intake resonator 22, the compressor/heat exchanger assembly 24, the feed and waste valves 40, 42, 44, 46, and sound absorbing muffler 48, these components according to the invention are mounted in a separate, removable module assembly 60 as will be described.
  • Referring now to FIG. 2, a front view of the reduced [0024] noise oxygen concentrator 20 is shown. The operating components of the apparatus are enclosed within an outer housing or cabinet 25, the front cover of which has been removed from this view to illustrate component module assembly 60. Attached to the outer surface of the module side walls 61 at both sides and the top wall 69 is a layer of sound deadening material 74. Also shown in FIG. 2 is a fan assembly panel 66. Additionally, a layer of sound deadening material is shown to be attached to the inner surface of the back wall 67 of the cabinet superstructure (not shown), where the outer surface of the back wall 67 of the module assembly 60 meets the inner surface of the back wall.
  • Referring again to FIG. 2, the working components shown to be mounted on the front side of the [0025] concentrator 20 within module 60 include intake resonator 22, fan 63, a valve block 64 forming the feed and waste valves 40, 42, 44, 46, and waste muffler 48. The working components of the back side of the concentrator as illustrated in FIG. 3 and partially in FIG. 2 include the pair of adsorbers 30 and 32, equalization valve 52, a circuit board 70 containing the electronic components that control the operating sequence of the apparatus 20, and compressor assembly 24. The compressor 24 is mounted to the bottom wall 62 of module 60 by means of the appropriate screws or other suitable fastening devices.
  • The [0026] valve block 64, as shown in FIG. 2 and FIG. 3, is disposed within module 60 immediately below and in front of the compressor assembly 24. The valve block 64 may suitably be attached to bottom wall 62 by means of a quick release fastener, such as Velcro™. The feed valves 30 a, 32 a are in the flow path between the heat exchanger 24 b and the adsorber inlets 30 a, 32 a by suitable tubing which at 71 and 72 are connected by detachable couplings to enable removal of the module 60. Although not illustrated, the electrical connections between the operating components within the module 60 on the one hand, and the power source and circuit board 70 on the other hand, also are made by detachable bus connections in a manner well known in the art.
  • Immediately above the [0027] bottom wall 62 of module 60 is the intake resonator 22. The intake resonator 22, as shown in FIG. 5, is mounted in close proximity to fan 63 to receive through filtered intake 21 (not shown) the portion of air to be fractionated. Ambient air is drawn into housing 25 by a suitable louvered opening (not shown) in the rear wall 67 of housing 25.
  • The [0028] upper wall 69 of component module assembly 60 has an opening 65 coinciding with the internal fan panel 66. The fan panel 66 is mounted at about a 20° angle so that fan 63 draws air from inside housing 25 into the component module assembly 60 to be directed partially into intake 21 and the balance over the operating components within module 60 before exiting through an opening at the back wall of module 60.
  • In furtherance of this objective the fan and compressor have been repositioned within the walls of the module to further reduce the noise level. This is accomplished by positioning the compressor substantially toward the back wall, opposing the [0029] fan panel 66.
  • FIG. 4 further illustrates the [0030] opening 65 in the top of the module 60 adjacent to the fan 63. FIG. 5a and FIG. 5b provide two views of the fan 63 and fan panel 66 and. further illustrate the means and angle by which fan 63 mounted to the fan panel 66. FIG. 5b further illustrates a layer of sound absorbing material 75 between the fan assembly panel 66 and the fan 63. The fan assembly panel 66 is then mounted between the sidewalls, angularly facing the opening in the upper wall. The noise reducing qualities of this device are further enhanced by the addition of a layer of sound absorbing material 75. This sound absorbing material will attenuate structure borne vibration and reduce radiated noise. Suitable openings (not shown) are provided in the modules walls, as for example bottom wall 62 and back wall 67 of the component module assembly 60 where the circulating air cooling the contained components and the waste gas from muffler 48 exit the component module assembly.
  • FIG. 6 is a the side view of the component module assembly with side cover removed. The figure particularly illustrates a [0031] compressor 24 mounted in close proximity to the back wall 67 of the component module assembly. The figure also illustrates a side view of the fan panel 66, mounted in close proximity to the front wall 68 of the component module assembly. Sounds normally associated with the discharging of a pressurized stream of gas to the atmosphere are muffled by the silencer 48.
  • While this invention has been described as having a particular design, the present invention can be further modified within the spirit and scope of this disclosure. This application is therefore intended to cover any variations, uses, or adaptations of the present invention using the general principles disclosed herein. Further, this application is intended to cover such departures from the present disclosure as come within the known or customary practice in the art to which this invention pertains and which fall within the limits of the appended claims. [0032]

Claims (6)

1. A pressure swing adsorption apparatus having operating components for producing a concentration of oxygen or other gas from a gas mixture such as ambient air, the apparatus comprising an housing containing the operating components and a component module assembly positioned within said housing, the component module assembly containing selected ones of the operating components and removably mounted within the housing.
2. The apparatus of claim 1, in which the selected ones of the operating components comprise those components generating higher levels of noise during operation.
3. The apparatus of claim 2 in which one of the selected components comprises a blower fan to draw the gas mixture into the module assembly and the module assembly includes wall means defining an opening in fluid communication with the blower fan.
4. The apparatus of claim 3 wherein others of the selected components comprise an intake resonator, a gas compressor, operating valves and an exhaust muffler, and the wall means further defines an opening to exhaust the portion of the gas mixture not forming part of the concentration of oxygen or other gas.
5. The apparatus of claim 3 in which the blower fan is affixed to the wall means, and further comprising a layer of sound and vibration absorbing material mounted between the blower fan and the wall means.
6. The apparatus of claim 2 wherein the module assembly comprises top, bottom, front, back and side walls enclosing the selected operating components, and further comprising at least one layer of sound absorbing material covering the outer surface of at least the top, front and side walls.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050204923A1 (en) * 2002-03-05 2005-09-22 Hitoshi Nakamura Oxygen enricher
US20110192122A1 (en) * 2010-02-09 2011-08-11 Invacare Corporation Breathing gas supply system
DE202010009330U1 (en) 2010-06-21 2011-10-20 Ai Mediq S.A. Device for complex hypoxia therapy
RU169867U1 (en) * 2016-04-22 2017-04-04 Александр Владимирович Гущин DEVICE FOR REMOVING OXYGEN FROM AIR
US9956371B2 (en) 2015-03-24 2018-05-01 Ventec Life Systems, Inc. Ventilator with integrated cough-assist
CN110709126A (en) * 2017-05-30 2020-01-17 艾诺根公司 Compact portable oxygen concentrator
US10773049B2 (en) 2016-06-21 2020-09-15 Ventec Life Systems, Inc. Cough-assist systems with humidifier bypass
US11191915B2 (en) 2018-05-13 2021-12-07 Ventec Life Systems, Inc. Portable medical ventilator system using portable oxygen concentrators
US11247015B2 (en) 2015-03-24 2022-02-15 Ventec Life Systems, Inc. Ventilator with integrated oxygen production

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE517673T1 (en) * 2003-09-02 2011-08-15 Airsep Corp SOUND HOUSING FOR PORTABLE OXYGEN CONCENTRATORS
JP4971582B2 (en) 2004-02-16 2012-07-11 帝人ファーマ株式会社 Oxygen concentrator
US8016925B2 (en) 2004-10-12 2011-09-13 Mccombs Norman R Mini-portable oxygen concentrator
US7954490B2 (en) 2005-02-09 2011-06-07 Vbox, Incorporated Method of providing ambulatory oxygen
US7402193B2 (en) 2005-04-05 2008-07-22 Respironics Oxytec, Inc. Portable oxygen concentrator
US7368005B2 (en) 2005-04-05 2008-05-06 Respironics Oxytec, Inc. Portable oxygen concentrator
US7329304B2 (en) 2005-04-05 2008-02-12 Respironics Oxytec, Inc. Portable oxygen concentrator
US7510601B2 (en) * 2005-12-20 2009-03-31 Air Products And Chemicals, Inc. Portable medical oxygen concentrator
WO2008004523A1 (en) * 2006-07-03 2008-01-10 Sanyo Electronic Industries Co., Ltd. Oxygen concentrating device
FR2906160B1 (en) 2006-09-25 2009-06-05 Air Liquide PSA METHOD WITH COMPOSITE ADSORPTION BED FORMED OF ADSORBENT AND AGGLOMERATS OF MCP
WO2008154273A2 (en) * 2007-06-08 2008-12-18 Sequal Technologies, Inc. Compressor cooling system and method of use
US20090065007A1 (en) 2007-09-06 2009-03-12 Wilkinson William R Oxygen concentrator apparatus and method
US8695600B2 (en) 2009-07-22 2014-04-15 Vbox, Incorporated Method of separating and distributing oxygen
US20120055474A1 (en) 2010-09-07 2012-03-08 Wilkinson William R Methods and systems for providing oxygen enriched gas
US8616207B2 (en) 2010-09-07 2013-12-31 Inova Labs, Inc. Oxygen concentrator heat management system and method
KR101200387B1 (en) * 2010-11-02 2012-11-12 주식회사 옥시젠클럽 Oxygen producing apparatus
US8440004B2 (en) * 2010-12-30 2013-05-14 Inogen, Inc. Advanced portable oxygen concentrator
WO2012136913A1 (en) 2011-04-08 2012-10-11 L'air Liquide,Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Mixture of an adsorbent and a phase change material with an adapted density
EP3998097A1 (en) 2012-04-05 2022-05-18 Fisher & Paykel Healthcare Limited Respiratory assistance apparatus
NZ707159A (en) 2012-10-12 2018-06-29 Inova Labs Inc Dual oxygen concentrator systems and methods
AU2013328916A1 (en) 2012-10-12 2015-05-14 Inova Labs, Inc. Oxygen concentrator systems and methods
WO2014059405A1 (en) 2012-10-12 2014-04-17 Inova Labs, Inc. Method and systems for the delivery of oxygen enriched gas
US9440179B2 (en) 2014-02-14 2016-09-13 InovaLabs, LLC Oxygen concentrator pump systems and methods
CN106535972B (en) 2014-05-27 2019-09-03 费雪派克医疗保健有限公司 Gas mixing and measurement for medical device
WO2017095241A2 (en) 2015-12-02 2017-06-08 Fisher & Paykel Healthcare Limited Flow path sensing for flow therapy apparatus
WO2017192660A1 (en) 2016-05-03 2017-11-09 Inova Labs, Inc. Method and systems for the delivery of oxygen enriched gas
US10843120B2 (en) 2016-06-29 2020-11-24 Koninklijke Philips N.V. Rotary valve assembly for pressure swing adsorption system
WO2019201631A1 (en) * 2018-04-16 2019-10-24 Parker Hannifin Emea S.À.R.L., A pressure swing adsorption system

Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144314A (en) * 1960-06-22 1964-08-11 Bell Telephone Labor Inc Means for supplying pressurized dry air to an enclosure and cable systems embodying such means
US3258899A (en) * 1962-02-06 1966-07-05 Puregas Equipment Corp Apparatus for fractionating gaseous mixtures
US3564816A (en) * 1968-12-30 1971-02-23 Union Carbide Corp Selective adsorption process
US3636679A (en) * 1971-01-04 1972-01-25 Union Carbide Corp Selective adsorption gas separation process
US3717974A (en) * 1968-12-30 1973-02-27 Union Carbide Corp Selective adsorption process for air separation
US3922149A (en) * 1974-01-30 1975-11-25 Garrett Corp Oxygen air enrichment method
US4302224A (en) * 1979-10-12 1981-11-24 Greene & Kellogg, Inc. Compact oxygen concentrator
US4342573A (en) * 1979-10-12 1982-08-03 Greene & Kellogg, Incorporated Compact oxygen concentrator
US4509959A (en) * 1983-07-28 1985-04-09 Greene & Kellogg, Inc. Modular industrial oxygen concentrator
US4559065A (en) * 1984-03-15 1985-12-17 Wilkerson Corporation Twin tower gas fractionation apparatus
US4584001A (en) * 1983-08-09 1986-04-22 Vbm Corporation Modular oxygen generator
US4802899A (en) * 1987-09-21 1989-02-07 Airsep Corporation Pressure swing adsorption apparatus
US4826510A (en) * 1988-01-13 1989-05-02 The John Bunn Company Portable low profile DC oxygen concentrator
US4971609A (en) * 1990-02-05 1990-11-20 Pawlos Robert A Portable oxygen concentrator
US5171336A (en) * 1991-06-17 1992-12-15 Shulick Robert J Purge air system
US5474595A (en) * 1994-04-25 1995-12-12 Airsep Corporation Capacity control system for pressure swing adsorption apparatus and associated method
US5531807A (en) * 1994-11-30 1996-07-02 Airsep Corporation Apparatus and method for supplying oxygen to passengers on board aircraft
US5871564A (en) * 1997-06-16 1999-02-16 Airsep Corp Pressure swing adsorption apparatus
US6036754A (en) * 1996-10-09 2000-03-14 Brian Walker Adsorption gas dryer
US20020029691A1 (en) * 2000-05-10 2002-03-14 Mccombs Norman R. Multiple bed pressure swing adsorption method and apparatus
US6478850B2 (en) * 2000-08-02 2002-11-12 Wearair Oxygen Inc. Miniaturized wearable oxygen concentrator

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3543482A (en) * 1967-05-01 1970-12-01 W D Gale Inc Air drier system
US4378982A (en) * 1981-08-28 1983-04-05 Greene & Kellogg, Inc. Compact oxygen concentrator
US4511377A (en) * 1983-11-01 1985-04-16 Greene & Kellogg, Inc. Apparatus for the production of oxygen

Patent Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144314A (en) * 1960-06-22 1964-08-11 Bell Telephone Labor Inc Means for supplying pressurized dry air to an enclosure and cable systems embodying such means
US3258899A (en) * 1962-02-06 1966-07-05 Puregas Equipment Corp Apparatus for fractionating gaseous mixtures
US3564816A (en) * 1968-12-30 1971-02-23 Union Carbide Corp Selective adsorption process
US3717974A (en) * 1968-12-30 1973-02-27 Union Carbide Corp Selective adsorption process for air separation
US3636679A (en) * 1971-01-04 1972-01-25 Union Carbide Corp Selective adsorption gas separation process
US3922149A (en) * 1974-01-30 1975-11-25 Garrett Corp Oxygen air enrichment method
US4302224A (en) * 1979-10-12 1981-11-24 Greene & Kellogg, Inc. Compact oxygen concentrator
US4342573A (en) * 1979-10-12 1982-08-03 Greene & Kellogg, Incorporated Compact oxygen concentrator
US4509959A (en) * 1983-07-28 1985-04-09 Greene & Kellogg, Inc. Modular industrial oxygen concentrator
US4584001A (en) * 1983-08-09 1986-04-22 Vbm Corporation Modular oxygen generator
US4559065A (en) * 1984-03-15 1985-12-17 Wilkerson Corporation Twin tower gas fractionation apparatus
US4802899A (en) * 1987-09-21 1989-02-07 Airsep Corporation Pressure swing adsorption apparatus
US4826510A (en) * 1988-01-13 1989-05-02 The John Bunn Company Portable low profile DC oxygen concentrator
US4971609A (en) * 1990-02-05 1990-11-20 Pawlos Robert A Portable oxygen concentrator
US5171336A (en) * 1991-06-17 1992-12-15 Shulick Robert J Purge air system
US5474595A (en) * 1994-04-25 1995-12-12 Airsep Corporation Capacity control system for pressure swing adsorption apparatus and associated method
US5531807A (en) * 1994-11-30 1996-07-02 Airsep Corporation Apparatus and method for supplying oxygen to passengers on board aircraft
US6036754A (en) * 1996-10-09 2000-03-14 Brian Walker Adsorption gas dryer
US5871564A (en) * 1997-06-16 1999-02-16 Airsep Corp Pressure swing adsorption apparatus
US20020029691A1 (en) * 2000-05-10 2002-03-14 Mccombs Norman R. Multiple bed pressure swing adsorption method and apparatus
US6478850B2 (en) * 2000-08-02 2002-11-12 Wearair Oxygen Inc. Miniaturized wearable oxygen concentrator

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050204923A1 (en) * 2002-03-05 2005-09-22 Hitoshi Nakamura Oxygen enricher
US7179326B2 (en) * 2002-03-05 2007-02-20 Teijin Limited Oxygen concentration apparatus
US20110192122A1 (en) * 2010-02-09 2011-08-11 Invacare Corporation Breathing gas supply system
WO2011100223A1 (en) * 2010-02-09 2011-08-18 Invacare Corporation Breathing gas supply system
EP2533862A1 (en) * 2010-02-09 2012-12-19 Invacare Corporation Breathing gas supply system
US8567396B2 (en) 2010-02-09 2013-10-29 Invacare Corp. Breathing gas supply system
AU2011215991B2 (en) * 2010-02-09 2013-11-14 Invacare Corporation Breathing gas supply system
EP2533862A4 (en) * 2010-02-09 2014-12-10 Invacare Corp Breathing gas supply system
DE202010009330U1 (en) 2010-06-21 2011-10-20 Ai Mediq S.A. Device for complex hypoxia therapy
US10105509B2 (en) 2015-03-24 2018-10-23 Ventec Life Systems, Inc. Active exhalation valve
US10758699B2 (en) 2015-03-24 2020-09-01 Ventec Life Systems, Inc. Secretion trap
US10046134B2 (en) 2015-03-24 2018-08-14 Ventec Life Systems, Inc. Pressure swing adsorption oxygen generator
US11344692B2 (en) 2015-03-24 2022-05-31 Ventec Life Systems, Inc. Respiratory therapy systems and methods
US10245406B2 (en) 2015-03-24 2019-04-02 Ventec Life Systems, Inc. Ventilator with integrated oxygen production
US10315002B2 (en) 2015-03-24 2019-06-11 Ventec Life Systems, Inc. Ventilator with integrated oxygen production
US10518059B2 (en) 2015-03-24 2019-12-31 Ventec Life Systems, Inc. Passive leak valve
US11291791B2 (en) 2015-03-24 2022-04-05 Ventee Life Systems, Inc. Ventilator with integrated cough-assist
US10576237B2 (en) 2015-03-24 2020-03-03 Ventec Life Systems, Inc. Active exhalation valve
US9956371B2 (en) 2015-03-24 2018-05-01 Ventec Life Systems, Inc. Ventilator with integrated cough-assist
US11247015B2 (en) 2015-03-24 2022-02-15 Ventec Life Systems, Inc. Ventilator with integrated oxygen production
US11185655B2 (en) 2015-03-24 2021-11-30 Ventec Life Systems, Inc. Passive leak valve
RU169867U1 (en) * 2016-04-22 2017-04-04 Александр Владимирович Гущин DEVICE FOR REMOVING OXYGEN FROM AIR
US10773049B2 (en) 2016-06-21 2020-09-15 Ventec Life Systems, Inc. Cough-assist systems with humidifier bypass
US11679229B2 (en) 2016-06-21 2023-06-20 Ventec Life Systems, Inc. Cough-assist systems with humidifier bypass
CN110709126A (en) * 2017-05-30 2020-01-17 艾诺根公司 Compact portable oxygen concentrator
US11191915B2 (en) 2018-05-13 2021-12-07 Ventec Life Systems, Inc. Portable medical ventilator system using portable oxygen concentrators

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US6908503B2 (en) 2005-06-21
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DE60312837T2 (en) 2007-12-06
EP1497012A1 (en) 2005-01-19
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DE60312837D1 (en) 2007-05-10
JP4398736B2 (en) 2010-01-13
EP1497012A4 (en) 2005-11-16
WO2003090903A1 (en) 2003-11-06
AU2003223693A1 (en) 2003-11-10
ATE357962T1 (en) 2007-04-15

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